CN113165357B - Reactive adhesive, laminate, and package - Google Patents

Abstract

A reactive adhesive comprising a polyol composition (A) and a polyisocyanate composition (B), characterized in that the polyol composition (A) comprises a polyester polyol (A1) and/or a polyester polyurethane polyol (A2) and has an average particle diameter of 1 x 10 ^‑3 A fine particle (C) having a diameter of not less than 0.5mm, wherein the polyester polyol (A1) is a reaction product obtained by charging polyethylene terephthalate, a polyol and a polybasic acid at one time, the polyester polyurethane polyol (A2) is a reaction product of the polyester polyol (A1) and an isocyanate compound, and the polyester polyurethane polyol (A) contains 1X 10 times the total resin solid content of the polyol composition (A) ^‑6 The fine particles (C) are contained in an amount of not less than 0.1 mass% by mass.

Description

Reactive adhesive, laminate, and package

Technical Field

The present invention relates to a reactive adhesive, and a laminate and a package using the same.

Background

Conventionally, laminates obtained by laminating (laminating) various plastic films to each other or plastic films, metal vapor-deposited films, and metal foils have been used in various applications, for example, in outdoor industrial applications such as packaging materials for foods, pharmaceuticals, and consumer goods, barrier materials, roofing materials, solar cell panel materials, battery packaging materials, window materials, outdoor flooring materials, illumination protection materials, automobile members, signboards, and labels, and in decorative applications such as injection molding and simultaneous decoration methods.

These laminates can be produced by appropriately combining various plastic films, metal vapor-deposited films, or metal foils in accordance with the properties required for various applications, and selecting an adhesive agent in accordance with the required properties. For example, in the case of foods and daily necessities, functions such as strength, resistance to cracking, boiling resistance, heat resistance, and resistance to contents physical properties are required in order to protect contents from various distribution, storage such as refrigeration, and treatment such as heat sterilization. Or in outdoor industrial applications, weather resistance and hydrolysis resistance are required for maintaining adhesion for a long period of time even in an open air environment.

Further, these laminated bodies rarely flow in a sheet form, and for example, they are formed into a bag shape with ends heat-sealed, or subjected to a molding process by thermoforming, and in some cases, heat sealability and moldability are required.

As an adhesive used for such lamination, a reactive adhesive (also referred to as a two-component adhesive) in which a hydroxyl group and isocyanate are reacted has been known.

For example, in food applications, an adhesive is known which contains a diol compound (a) having 2 hydroxyl groups and a polyisocyanate (B) having 2 or more isocyanate groups, wherein the number average molecular weight (Mn) of the diol compound (a) is in the range of 400 to 3000, and the polyisocyanate (B) is a mixture of a 3-or more-membered polyisocyanate compound (B1) and a diisocyanate compound (B2) obtained by adding an isocyanate compound to a polyester diol (see, for example, patent document 1).

A laminating adhesive for a laminated film of a battery packaging material is known, which contains a polyurethane polyol having a polyol component with a number average molecular weight of 5000 or more and less than 14000, and which has excellent molding processability and moist heat resistance, wherein the sum of the content of urethane bonds and the content of isocyanate groups is within a specific range (see, for example, patent document 2).

These reactive adhesives are required to have properties corresponding to various uses, for example, adhesives before mixing of two components are required to have storage stability with time (this means that they can withstand outdoor temperature when stored in a warehouse or the like, and particularly can withstand high temperature in summer); from the viewpoint of productivity, for example, a laminate is required to have a coating speed of 200 m/min or more, and to have no appearance defects or the like. However, under such high-speed coating (also referred to as high-speed processing) conditions, there is a problem that a solvent-free reactive adhesive not using an organic solvent is liable to cause orange peel-like appearance defects depending on the substrate, even in the case of a dry laminate type reactive adhesive whose viscosity can be adjusted using an organic solvent.

Documents of the prior art

Patent document

Patent document 1: japanese unexamined patent publication No. 2014-101422

Patent document 2: japanese laid-open patent publication No. 2016-196580

Patent document 3: japanese patent laid-open publication No. 2002-3815

Patent document 4: japanese patent application laid-open No. 2010-248345

Disclosure of Invention

Problems to be solved by the invention

The problem to be solved by the present invention is to provide a reactive adhesive which can be used as an adhesive for a laminate formed by appropriately combining various plastic films, metal vapor-deposited films, or metal foils, has excellent storage stability over time, and can provide a laminate having high adhesion and excellent appearance after lamination even under high-speed coating conditions.

Means for solving the problems

The present inventors have found that a reactive adhesive, which is characterized in that,the adhesive is a reactive adhesive comprising a polyol composition (A) and a polyisocyanate composition (B), wherein the polyol composition (A) contains a polyester polyol (A1) and 1X 10 relative to the total resin solids content of the polyol composition (A) ^-6 An average particle diameter of 1X 10 mass% or more and less than 0.1 mass% ^-3 And fine particles (C) having a diameter of not less than 0.5mm, wherein the polyester polyol (A1) is a reaction product obtained by charging polyethylene terephthalate, a polyol and a polybasic acid at one time.

Adhesives using polyester polyols made of polyethylene terephthalate are known (see, for example, patent documents 3 and 4). For example, patent document 3 discloses a reactive adhesive containing a polyester polyol obtained by decomposing polyethylene terephthalate in a reaction with a low-molecular polyol and then subjecting the decomposed product to a condensation reaction with a polybasic acid, and a polyisocyanate curing agent. However, although patent document 3 evaluates a laminate film produced by applying an adhesive at a film speed of 50m/min, it does not describe or teach a form produced under high-speed application conditions at an application speed of 200 m/min or more. Patent document 4 discloses the use of a polyol compound obtained by depolymerization of a polyester (a) with a polyol (b) having 2 or more hydroxyl groups in 1 molecule as a raw material of an adhesive, but it also evaluates a laminated film obtained by laminating a film coated with a film thickness of 30 μm on a film with a coater as an adhesive, and does not describe or teach a mode of production under high-speed coating conditions at a coating speed of 200 m/min or more at all. That is, in practice, even when a polyester polyol using polyethylene terephthalate as a raw material is used, a reactive adhesive having high adhesiveness and excellent appearance after lamination processing under high-speed coating conditions at a coating speed of 200 m/min or more has not been developed.

The present inventors have understood that the polyester polyols obtained by the methods disclosed in patent documents 3 and 4 have poor appearance when coated at high speed, and have found that the polyester polyols obtained by the methods disclosed in patent documents 3 and 4 contain polyethylene terephthalate, a polyol and a polybasic acid, and the polyester polyols are added at onceThe polyester polyol (A1) which is the reaction product obtained in the above manner and the total resin solids content of the above polyol composition (A) are 1X 10 ^-6 An average particle diameter of 1X 10 mass% or more and less than 0.1 mass% ^-3 The polyol composition (a) of fine particles (C) having a size of not less than 0.5mm is excellent in storage stability with time, is less likely to cause appearance defects in high-speed coatability, and can provide a laminate having high adhesiveness after lamination, particularly heat resistance and content resistance.

That is, the present invention provides a reactive adhesive comprising a polyol composition (a) and a polyisocyanate composition (B), wherein the polyol composition (a) comprises a polyester polyol (A1) which is a reaction product obtained by charging polyethylene terephthalate, a polyol and a polybasic acid at one time and/or a polyester polyurethane polyol (A2) which is a reaction product of the polyester polyol (A1) and an isocyanate compound, and a reactive adhesive having an average particle diameter of 1 × 10 ^-3 Fine particles (C) of not less than 0.5mm,

the polyol composition (A) contains 1X 10 of the total resin solids content ^-6 At least 0.1 mass% of the fine particles (C).

The present invention also provides a laminate comprising a first plastic film and a second plastic film, and an adhesive layer laminated between the first plastic film and the second plastic film, wherein the adhesive layer is a layer of the above-described reactive adhesive.

The present invention also provides a laminate comprising a first plastic film, a printing layer, an adhesive layer and a second plastic film laminated in this order, wherein the adhesive layer is a layer of the reactive adhesive described above.

The present invention also provides a package obtained by forming the laminate described above into a bag shape.

The present invention also provides a method for producing a polyester polyol (A1), which comprises: a step of adding polyethylene terephthalate, a polyhydric alcohol and a polybasic acid at once to react them, and then filtering them with a filter.

The present invention also provides a method for producing a polyester-polyurethane polyol (A2), comprising: a step of reacting a polyester polyol (A1) obtained by once charging and reacting polyethylene terephthalate, a polyol and a polybasic acid with a polyisocyanate, and then filtering the reaction product with a filter.

Effects of the invention

The reactive adhesive of the present invention is useful as an adhesive for a laminate in which various plastic films, metal vapor-deposited films, or metal foils are appropriately combined, has excellent storage stability over time, and can provide a laminate having high adhesiveness and excellent appearance after lamination even under high-speed coating conditions. Further, it is excellent in heat resistance and content resistance, and therefore, it is particularly preferable for use as a food packaging bag.

Detailed Description

The present invention is a reactive adhesive comprising a polyol composition (A) and a polyisocyanate composition (B), wherein the polyol composition (A) comprises a polyester polyol (A1) which is a reaction product obtained by charging polyethylene terephthalate, a polyol and a polybasic acid all at once and/or a polyester urethane polyol (A2) which is a reaction product of the polyester polyol (A1) and an isocyanate compound, and a reactive adhesive having an average particle diameter of 1X 10 ^-3 Fine particles (C) of not less than 0.5mm,

the polyol composition (A) contains 1X 10 of the total resin solids content ^-6 At least 0.1 mass% of the fine particles (C).

(polyol composition (A))

The polyester polyol (A1) contained in the polyol composition (a) is a reaction product obtained by once charging polyethylene terephthalate, a polyol and a polybasic acid.

(polyester polyol (A1))

The polyethylene terephthalate (hereinafter, sometimes referred to as PET) used in the present invention may be obtained by polycondensation of terephthalic acid or dimethyl terephthalate and ethylene glycol, and may be modified with isophthalic acid, phthalic anhydride, adipic acid, cyclohexanedicarboxylic acid, 1, 3-butanediol, cyclohexanedimethanol, or the like, if necessary. Further, it is possible to use: PET obtained by crushing commercially available unused PET bottles, PET films, and defective products in the production of other PET products, recycled PET obtained by recovering and washing waste, and the like. Among them, recycled PET is preferably used. For these, PET which has been washed and granulated is commercially available.

The Intrinsic Viscosity (IV) of PET is preferably from 0.50 to 0.80 dL/g. By within this range, the polycondensation reaction of PET with other raw materials can be carried out at 250 ℃ or lower. In addition, the reactive adhesive containing the polyester polyol containing PET is also preferably in this range from the viewpoint of exhibiting adhesive strength, durability, and heat resistance.

The polyol used in the present invention is not particularly limited, and known polyols can be used.

Examples thereof include: aliphatic diols such as 1, 2-propanediol, 1, 2-trimethyl-1, 3-propanediol, 2-dimethyl-3-isopropyl-1, 3-propanediol, 1, 3-butanediol, and 2, 4-trimethyl-1, 3-pentanediol; alicyclic diols such as 1, 3-bis (2-hydroxypropyl) cyclopentane, 1, 3-bis (2-hydroxybutyl) cyclopentane, 1, 4-bis (2-hydroxypropyl) cyclohexane, and 1, 4-bis (2-hydroxybutyl) cyclohexane; aromatic diols such as 1, 4-bis (2-hydroxypropyl) benzene and 1, 4-bis (2-hydroxybutyl) benzene;

alkylene oxide adducts of bisphenols obtained by adding a bisphenol such as 2, 2-bis (4-hydroxyphenyl) propane (hereinafter, abbreviated as "bisphenol a"), 2-bis (4-hydroxyphenyl) butane (hereinafter, abbreviated as "bisphenol B"), bis (4-hydroxyphenyl) methane (hereinafter, abbreviated as "bisphenol F"), bis (4-hydroxyphenyl) sulfone (hereinafter, abbreviated as "bisphenol S") to an alkylene oxide having a secondary hydroxyl group such as 1, 2-propylene oxide or 1, 2-butylene oxide; aliphatic polyhydric alcohols such as ethylene glycol, diethylene glycol, 1, 3-propanediol, 1, 4-butanediol, 3-methyl-1, 3-butanediol, 1, 5-pentanediol, 3-methyl-1, 5-pentanediol, neopentyl glycol, 2-butyl-2-ethyl-1, 3-propanediol, 1, 6-hexanediol, trimethylolethane, trimethylolpropane, glycerol, hexanetriol, pentaerythritol and the like; ether glycols such as polyoxyethylene glycol and polyoxypropylene glycol;

modified polyether polyols obtained by ring-opening polymerization of the above aliphatic polyols with various compounds having a cyclic ether bond such as ethylene oxide, propylene oxide, tetrahydrofuran, ethyl glycidyl ether, propyl glycidyl ether, butyl glycidyl ether, phenyl glycidyl ether and allyl glycidyl ether; lactone polyester polyols obtained by polycondensation of the above aliphatic polyols with various lactones such as epsilon-caprolactone; bisphenols such as bisphenol a, bisphenol F and bisphenol S; ethylene oxide adducts of bisphenols obtained by adding ethylene oxide to bisphenols such as bisphenol a and bisphenol F.

These may be used alone or in combination of 2 or more. Among them, aliphatic polyhydric alcohols such as ethylene glycol, diethylene glycol, 1, 3-propanediol, 1, 4-butanediol, 3-methyl-1, 3-butanediol, 1, 5-pentanediol, 3-methyl-1, 5-pentanediol, neopentyl glycol, 2-butyl-2-ethyl-1, 3-propanediol, 1, 6-hexanediol, trimethylolethane, trimethylolpropane, glycerol, hexanetriol and pentaerythritol are preferable, and 1, 6-hexanediol is more preferable.

The polybasic acid used in the present invention is not particularly limited, and any known polybasic acid can be used.

Examples thereof include: aromatic dicarboxylic acids such as phthalic acid, phthalic anhydride, terephthalic acid, isophthalic acid, and phthalic acid; aliphatic dicarboxylic acids such as malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, hexahydrophthalic acid, and 1, 4-cyclohexanedicarboxylic acid; aliphatic unsaturated dicarboxylic acids such as maleic acid, maleic anhydride, citraconic acid, dimethyl maleic acid, cyclopentene-1, 2-dicarboxylic acid, 1-cyclohexene-1, 2-dicarboxylic acid, 4-cyclohexene-1, 2-dicarboxylic acid, fumaric acid, mesaconic acid, itaconic acid, glutaconic acid, and the like; aliphatic tricarboxylic acids such as 1,2, 5-hexanetricarboxylic acid and 1,2, 4-cyclohexanetricarboxylic acid; aromatic tricarboxylic acids such as trimellitic acid, 1,2, 5-benzenetricarboxylic acid and 2,5, 7-naphthalene tricarboxylic acid, and dimer acid. These may be used alone or in combination of 2 or more. Dimer acid is also preferred.

The production method of putting PET, polyol and polybasic acid at once and reacting them can be optionally produced by a known polycondensation reaction method, and specifically, PET, polyol and polybasic acid are put into a production apparatus, heated to 180 ℃ or higher under stirring in a nitrogen atmosphere, and subjected to any production method such as atmospheric dehydration reaction, reduced-pressure and vacuum dehydration reaction, solution polycondensation method, solid phase polycondensation reaction, and the like. When the PET, the polyol and the polybasic acid described herein are used, the dehydration reaction under reduced pressure can be applied at a reaction temperature of 230 ℃ or less, and the reaction time can be set to about 5 hours. The progress of the polycondensation reaction can be confirmed by measuring the acid value, hydroxyl value, viscosity, or softening point. As the production apparatus used in this case, for example, a batch-type production apparatus such as a reaction vessel equipped with a nitrogen gas inlet, a thermometer, a stirrer, a rectifying column, etc. can be preferably used, and an extruder equipped with a vent, a continuous reaction apparatus, a kneader, etc. can be also used. If necessary, an esterification catalyst (tin compound, titanium compound, zirconium compound, etc.) may be further used to promote the esterification reaction.

In addition, in the method of subjecting PET to transesterification in a polyol and the polyol obtained by the method of polycondensing the transesterification reaction product with a polybasic acid, the ethylene terephthalate units are decomposed in a scattered manner, and therefore, even when the polyol is used for an adhesive, the appearance, adhesive strength, heat resistance and content resistance properties at the time of high-speed coating, which are the objects of the present invention, cannot be achieved.

(preferred combinations of raw materials)

Among the above polyester polyols (A1), those using 1, 6-hexanediol as the polyol and dimer acid as the polybasic acid are preferred. In this case, the weight fraction of 1, 6-hexanediol is preferably 5 to 20 mass%, more preferably 6 to 18 mass%, in terms of the ratio occupied by the polyester polyol (A1) as a charged raw material. The weight fraction of the dimer acid is preferably 5 to 20 mass%, more preferably 6 to 18 mass%, based on the ratio of the polyester polyol (A1) to the raw materials charged.

The PET is preferably 5 to 50% by mass, more preferably 8 to 48% by mass, based on 100% by mass of the total amount of the polyhydric alcohol and the polybasic acid, relative to the charged raw materials (i.e., the total amount of the polyhydric alcohol and the polybasic acid) of the polyester polyol (A1).

In the present application, an adhesive having more excellent adhesive strength to a substrate, heat resistance and content resistance can be obtained by synthesizing a long-chain unsaturated dibasic acid such as dimer acid, 1, 6-hexanediol, and other monomers together with PET as raw materials of the polyester polyol (A1). The reason for this is not clear, and it is presumed that if the composition is such that the reaction temperature is 220 ℃, the ethylene terephthalate unit in the reaction product obtained thereby becomes difficult to decompose due to the long-chain unsaturated group, remains in a state of being maintained in a high molecular weight body, and is presumed to contribute to appearance, adhesive strength, heat resistance and content resistance properties at the time of high-speed coating. In addition, as the polyol, in the case of a triol (trimethylolpropane), there is a possibility that the ethylene terephthalate unit in PET is sufficiently decomposed, and the reaction does not proceed if the reaction temperature is not higher than 220 ℃, and therefore the polyol is preferably a diol such as 1, 6-hexanediol.

(acid value, hydroxyl value)

The polyester polyol (A1) preferably has an acid value of 5.0 or less from the viewpoint of hydrolysis resistance, and more preferably 3.0 or less from the viewpoint of reactivity of the adhesive. From the viewpoint of high-speed coatability, the hydroxyl value is preferably 50 or less, more preferably 40 or less.

In the present invention, the acid value and the hydroxyl value are measured by the following methods, and unless otherwise specified, they are expressed as values in terms of solid content.

(acid value)

5 to 10g of polyester polyol was weighed into a 100ml Erlenmeyer flask. The weighed amount is set to (S). This was dissolved in 30ml of tetrahydrofuran. After 2 to 3 drops of phenolphthalein was added as an indicator, titration was carried out using 0.1mol/L potassium hydroxide alcoholic solution. The acid value was calculated from the titration amount (V) at the end of the time when the reddish color lasted for 30 seconds by the following equation. Further, the titer of the 0.1mol/L potassium hydroxide alcoholic solution was set to (F).

Acid value = (V × F × 5.61)/S

(hydroxyl value)

6 to 10g of polyester polyol was weighed into a 300ml Erlenmeyer flask. The weighed amount is set to (S). 25ml of the acetylating agent prepared in advance was added thereto and dissolved. A cooling tube was attached to the mouth of the Erlenmeyer flask, and acetylation was carried out at 100 ℃ for 1 hour. 10ml of ion-exchanged water was added thereto and the mixture was cooled to room temperature. 2 to 3 drops of phenolphthalein were added as an indicator, and then titration was performed with 0.5mol/L potassium hydroxide alcoholic solution. The hydroxyl value was calculated from the titration amount (V) at the time point when reddish color lasting 30 seconds was obtained as an end point by the following equation. A blank test was also performed, and the titration amount at this time was defined as (B). The titer of the 0.5mol/L potassium hydroxide alcoholic solution was set to (F). Separately, the acid value was measured in advance.

Hydroxyl value = ((B-V) × F × 28.05)/S + acid value

(molecular weight)

The number average molecular weight of the polyester polyol (A1) is not particularly limited, but is usually adjusted to a range of 2000 to 12000, preferably 3000 to 8000, from the viewpoint of an appropriate resin viscosity at the time of coating.

In the present invention, the number average molecular weight (Mn) and the weight average molecular weight (Mw) are values measured by Gel Permeation Chromatography (GPC) under the following conditions.

Measurement device: HLC-8220GPC, manufactured by Tosoh corporation

Column: TSK-GUARDCOLUMN SuperHZ-L manufactured by Tosoh corporation

+ Tosoh corporation TSK-GEL SuperHZM-Mx 4

A detector: RI (differential refractometer)

Data processing: multi Station GPC-8020model II, manufactured by Tosoh corporation

The measurement conditions were as follows: column temperature 40 deg.C

Solvent tetrahydrofuran

Flow rate 0.35 ml/min

And (3) standard: monodisperse polystyrene

Sample preparation: the resulting tetrahydrofuran solution was filtered through a microfilter at 0.2 mass% in terms of solid content of the resin (100. Mu.l)

(polyester polyurethane polyol (A2))

The polyester polyol (A2) contained in the polyol composition (a) is a polyester polyurethane polyol (A2) obtained by obtaining the polyester polyol (A1) and then further reacting the polyester polyol with an isocyanate compound.

The isocyanate compound used in the present invention may be any known compound without any particular limitation, and may be used alone or in combination of two or more. Examples thereof include: polyisocyanates having an aromatic structure in the molecular structure, such as toluene diisocyanate, diphenylmethane diisocyanate, polymeric diphenylmethane diisocyanate, 1, 5-naphthalene diisocyanate, triphenylmethane triisocyanate and xylylene diisocyanate, and compounds in which a part of the isocyanate groups (sometimes referred to as NCO groups) of these polyisocyanates is modified with carbodiimide;

allophanate (Allophanate) compounds derived from these polyisocyanates; polyisocyanates having an alicyclic structure in the molecular structure, such as isophorone diisocyanate, 4' -methylenebis (cyclohexyl isocyanate), and 1,3- (isocyanatomethyl) cyclohexane; linear aliphatic polyisocyanates such as 1, 6-hexamethylene diisocyanate, lysine diisocyanate, and trimethylhexamethylene diisocyanate, and allophanate compounds thereof; isocyanurate bodies of these polyisocyanates; allophanates derived from these polyisocyanates; biuret bodies derived from these polyisocyanates; a trimethylolpropane modified adduct;

polyisocyanates which are reaction products of the above-mentioned various polyisocyanate compounds with polyols, and the like.

Among them, diisocyanate is preferable, and isophorone diisocyanate is most preferable from the viewpoint of reaction stability.

The acid value of the polyester-polyurethane polyol (A2) is preferably 5.0 or less from the viewpoint of hydrolysis resistance, and more preferably 3.0 or less from the viewpoint of reactivity of the adhesive. From the viewpoint of heat resistance and internal resistance, the hydroxyl value is preferably 30 or less, more preferably 25 or less.

(Fine particle (C))

The fine particles (C) contained in the polyol composition (A) have an average particle diameter of 1X 10 ^-3 Fine particles (C) having a size of not less than 0.5 mm.

In the present invention, the average particle diameter is an average particle diameter measured by the following method.

[ average particle diameter of Fine particles ]

The polyol composition in which the fine particles are dispersed is diluted with an appropriate solvent, and the diluted solution is used to measure the average particle diameter on a volume basis by a laser light scattering method (laser diffraction particle size distribution measuring apparatus SALD-2300 (Shimadzu corporation)). When the fine particles are added, the refractive index inherent to the fine particles is used. In the case of fine particles contained in advance in polyethylene terephthalate, the refractive index was measured to be 1.4.

When the average particle diameter of the fine particles (C) is large and exceeds 0.5mm, the storage stability may deteriorate with time. Wherein the average particle diameter is 1 × 10 ^-3 more preferably not less than 0.4mm, 1X 10 ^-3 Preferably, the thickness is not less than 0.3 mm.

The fine particles (C) may be fine particles mainly composed of either an organic compound or an inorganic compound, and an organic compound is particularly preferable. Among them, organic high molecular compounds are preferable, and examples thereof include: examples of the fine particles include polyester resin fine particles, polyurethane resin fine particles, polyolefin resin fine particles such as polyethylene, polybutene, and polypropylene, polymer fine particles including styrene and polyolefin, fine particles including hydrogenated products thereof, cellulose resin fine particles, silicone resin fine particles, melamine resin fine particles, acrylic resin fine particles (for example, polymethyl methacrylate resin fine particles), acrylic-styrene copolymer fine particles, polycarbonate resin fine particles, polystyrene resin fine particles, and benzoguanamine resin fine particles. Further, these resins may be combined to form a composite. These crosslinkable groups may be non-crosslinkable groups, and are not particularly limited. Examples of the other organic compounds include organic pigments. Examples of the inorganic compound include: inorganic fillers such as silica, alumina, mica, talc, aluminum flakes and glass flakes, and lamellar inorganic compounds. The fine particles containing an organic compound or an inorganic compound as a main component may be used alone in 1 kind, or may be used in combination with 2 or more kinds.

The fine particles (C) contain 1X 10 of the total resin solids content of the polyol composition (A) ^-3 The content is preferably not less than 0.1% by mass. A reactive adhesive which is excellent in storage stability with time and can give a laminate having high adhesiveness and excellent appearance after lamination even under high-speed coating conditions. Wherein the content is 1 × 10 ^-6 More preferably not less than 0.08% by mass, 1X 10 ^-3 More preferably, the content is not less than 0.05% by mass.

The fine particles (C) may be added in a desired amount after the synthesis of the polyester polyol (A1) which is the main component of the polyol composition (a), or may be added in advance when the polyester polyol (A1) is reacted. When the fine particles are added using a commercially available product, the fine particles other than the average particle diameter corresponding to the fine particles (C) can be removed by filtration or the like. In the present invention, polyethylene terephthalate is used as a raw material of the polyester polyol (A1), and fine particles previously contained in the polyethylene terephthalate may be used. In particular, when PET obtained by pulverizing a defective product in the production of a commercially available unused PET bottle, PET film, or other PET product, or recycled PET recovered from waste and washed is used, many fine particles including an average particle diameter corresponding to the above fine particles (C) can be used. When the fine particles previously contained in the polyethylene terephthalate are used, fine particles other than the average particle diameter corresponding to the fine particles (C) can be removed by filtration or the like. The content can be set to a desired content by measuring the amount of fine particles contained in advance in the polyethylene terephthalate and using the polyethylene terephthalate containing a desired amount as a raw material.

When the content of fine particles contained in advance in polyethylene terephthalate is unknown, the content can be determined by measuring the Turbidity of a solution obtained by diluting a polyol composition with an appropriate solvent in Nephelometric Turbidity units "NTU (Nephelometric Turbidity Unit)" and converting the Turbidity into a mass.

Specific methods of filtration and the like include: the particulates are removed by filtration using a filter or filter paper. In addition, it is also possible to use: sedimentation by centrifugal separation or the like, precipitation by cooling, or the like. Among them, filtration with a filter is particularly preferable because the filtration step is the simplest and most convenient. Specifically, a polyester polyol (A1) containing a reaction product obtained by charging polyethylene terephthalate, a polyol and a polybasic acid all at once and reacting them is obtained by a single charge, and then filtered through a filter, and 1 × 10 relative to the total resin solid content of the polyol composition (a), the polyester polyol (A1) containing the reaction product obtained by charging polyethylene terephthalate, a polyhydric alcohol and a polybasic acid all at once ^-6 An average particle diameter of 1X 10 mass% or more and less than 0.1 mass% ^-3 Fine particles (C) of not less than 0.5mm in diameter.

Examples of the material of the filter used herein include: and fibers such as polypropylene, polyester, polyethylene, polypropylene, rayon, nylon, fluororesin, and cellulose, glass fibers, and those containing these fibers impregnated with a phenol resin or an epoxy resin. In addition, these may be used in combination. The mesh size of the filter is preferably 5 μm which is usually used, but is not particularly limited. Specifically, there may be mentioned: cuno Filter card manufactured by Nihon Pall (model: 5RPN19.5, material: polyester fiber impregnated with phenol resin), cuno Filter card manufactured by Nihon Pall (model: XFRPN19.5, material: polyester fiber impregnated with phenol resin), and the like. The filtration can be repeated by circulation filtration or the like until the particles become the target average particle diameter and content.

(other polyols)

In the present invention, the polyol itself, a polymer polyol selected from polyester polyols not using polyethylene terephthalate as a raw material, polyether polyols, polyurethane polyols, polyether polyols, polyester (polyurethane) polyols, polyether (polyurethane) polyols, polyesteramide polyols, acrylic polyols, polycarbonate polyols, polyhydroxyalkanes, castor oil, and mixtures thereof, may be used in addition to the polyester polyol (A1) within a range not impairing the effects of the present invention.

When other polyols are used in combination, the proportion of the polyester polyol (A1) in the polyol composition (A) is preferably from 1 to 50% by mass, more preferably from 1 to 40% by mass.

(polyisocyanate composition (B))

The polyisocyanate composition (B) used in the present invention is a composition containing a polyisocyanate compound as a main component. The polyisocyanate compound used in the present invention may be any known compound without any particular limitation, and may be used alone or in combination of two or more. Examples thereof include: polyisocyanates having an aromatic structure in the molecular structure, such as toluene diisocyanate, diphenylmethane diisocyanate, polymeric diphenylmethane diisocyanate, 1, 5-naphthalene diisocyanate, triphenylmethane triisocyanate and xylylene diisocyanate, and compounds in which a part of the isocyanate groups (sometimes referred to as NCO groups) of these polyisocyanates is modified with carbodiimide;

urea formate (Allophanate) compounds derived from these polyisocyanates; polyisocyanates having an alicyclic structure in the molecular structure, such as isophorone diisocyanate, 4' -methylenebis (cyclohexyl isocyanate), and 1,3- (isocyanatomethyl) cyclohexane; linear aliphatic polyisocyanates such as 1, 6-hexamethylene diisocyanate, lysine diisocyanate, and trimethylhexamethylene diisocyanate, and urea formate compounds thereof; isocyanurate bodies of these polyisocyanates; allophanates derived from these polyisocyanates; biuret bodies derived from these polyisocyanates; a trimethylolpropane modified adduct;

polyisocyanates as reaction products of the above-mentioned various polyisocyanate compounds with polyols, and the like.

Among the polyisocyanates which are reaction products of the various polyisocyanate compounds described above with polyols, the polyols may be used: the polyol used as a raw material of the polyol composition (a), the polyester polyol (A1), and a polymer polyol selected from polyester polyols, polyether polyols, polyurethane polyols, polyetherester polyols, polyester (polyurethane) polyols, polyether (polyurethane) polyols, polyesteramide polyols, acrylic polyols, polycarbonate polyols, polyhydroxyalkanes, castor oil, and mixtures thereof, which do not use polyethylene terephthalate as a raw material. Among them, the polyisocyanate which is a reaction product of the above-mentioned various polyisocyanates and the above-mentioned polyester polyol (A1) is preferably used from the viewpoint of adhesive strength, heat resistance and content resistance.

From the viewpoint of the balance between the cohesive force and flexibility of the adhesive coating film, the reaction ratio of the polyisocyanate compound and the polyol is preferably in the range of 1.0 to 5.0 in terms of the equivalent ratio of isocyanate groups to hydroxyl groups [ isocyanate group/hydroxyl group ].

From the viewpoint of adhesive strength, heat resistance and content resistance, the polyisocyanate compound preferably has an average molecular weight in the range of 100 to 1000.

(solvent)

The reactive adhesive used in the present invention is an adhesive that is cured by a chemical reaction between an isocyanate group and a hydroxyl group, and can be used as a solvent-type or solvent-free adhesive. The "solvent" of the solvent-free adhesive of the present invention means: the "solvent-free" means that the organic solvent having high solubility in which the polyisocyanate compound or the polyol compound used in the present invention can be dissolved is not included. Specific examples of the highly soluble organic solvent include: toluene (tolumene), xylene (xylene), methylene chloride, tetrahydrofuran, methanol, ethanol, isopropanol, methyl acetate, ethyl acetate, n-butyl acetate, acetone, methyl Ethyl Ketone (MEK), cyclohexanone, toluene (toluol), xylene (xylol), n-hexane, cyclohexane, and the like. Among them, toluene (tolumene), xylene (xylene), methylene chloride, tetrahydrofuran, methyl acetate, and ethyl acetate are known as organic solvents having particularly high solubility.

On the other hand, when the adhesive of the present invention requires a low viscosity or the like, it can be diluted with the above-mentioned organic solvent having high solubility and used appropriately according to the desired viscosity. At this time, either one of the dilutable polyisocyanate composition (B) or the polyol composition (a) may also dilute both. Examples of the organic solvent used in such a case include: methanol, ethanol, isopropanol, methyl acetate, ethyl acetate, n-butyl acetate, acetone, methyl Ethyl Ketone (MEK), cyclohexanone, toluene (tolol), xylene (xylol), n-hexane, cyclohexane, and the like. From the viewpoint of solubility, ethyl acetate and Methyl Ethyl Ketone (MEK) are preferred among these, and ethyl acetate is particularly preferred. The amount of the organic solvent to be used varies depending on the desired viscosity, and is usually in the range of about 20 to 50% by mass.

In the reactive adhesive used in the present invention, the blending ratio of the polyisocyanate composition (B) and the polyol composition (a) is preferably in the range of 0.6 to 5.0 in the equivalent ratio of isocyanate groups in the polyisocyanate compound contained in the polyisocyanate composition (B) to hydroxyl groups in the polyol compound contained in the polyol composition (a) [ isocyanate groups/hydroxyl groups ], from the viewpoint of excellent adhesive strength and heat resistance at the time of heat sealing, and particularly preferably in the range of 1.0 to 3.5 from the viewpoint of remarkable these properties.

(aliphatic cyclic amide Compound)

As described in detail, the reactive adhesive of the present invention contains the polyol composition (a) and the polyisocyanate composition (B) as essential components, but further contains an aliphatic cyclic amide compound in any one of the polyol composition (a) and the polyisocyanate composition (B) or in the form of a third component during coating, whereby it is possible to effectively suppress elution of harmful low-molecular-weight chemical substances such as aromatic amines into the contents of the laminated packaging body.

Examples of the aliphatic cyclic amide compound used herein include: delta-valerolactam, epsilon-caprolactam, omega-enantholactam, eta-caprylolactam, beta-propiolactam, and the like. Among these, epsilon-caprolactam is preferable from the viewpoint of having an excellent effect of reducing the amount of elution of low-molecular-weight chemical substances. Further, the amount of the aliphatic cyclic amide compound is preferably in the range of 0.1 to 5 parts by mass per 100 parts by mass of the polyol component a.

(catalyst)

In the present invention, the use of the catalyst can effectively suppress elution of harmful low-molecular-weight chemical substances such as aromatic amines into the contents of the laminated packaging body.

The catalyst used in the present invention is not particularly limited as long as it is used for promoting the urethanization reaction, and examples thereof include: metal catalysts, amine catalysts, diazabicycloundecene (DBU), aliphatic cyclic amide compounds, titanium chelate compounds, and the like.

Examples of the metal-based catalyst include: the metal complex is specifically an acetylacetone salt of a metal selected from the group consisting of Fe (iron), mn (manganese), cu (copper), zr (zirconium), th (thorium), ti (titanium), al (aluminum), sn (tin), zn (zinc), bi (bismuth), and Co (cobalt), and examples thereof include: iron acetylacetonate (Fe (acac)) is one of iron acetylacetonate, manganese acetylacetonate, copper acetylacetonate and zirconium oxide acetylacetonate, from the viewpoint of toxicity and catalyst activity ₃ ) Or manganese acetylacetonate (Mn (acac) ₂ ) Preferably, it is used.

Examples of the inorganic metal-based catalyst include: a catalyst selected from the group consisting of Fe, mn, cu, zr, th, ti, al, sn, zn, bi, co, and the like.

Examples of the organometallic catalyst include: stannous acetate, stannous octoate, stannous oleate, stannous laurate, dibutyltin oxide, dibutyltin diacetate, dibutyltin dilaurate, dibutyltin dichloride, dioctyltin dilaurate, nickel octoate, nickel naphthenate, cobalt octoate, cobalt naphthenate, bismuth octoate, bismuth naphthenate, bismuth neodecanoate, and the like. Among these, preferred compounds are organotin catalysts, and stannous octoate and dibutyltin dilaurate are more preferred.

The tertiary amine catalyst is not particularly limited as long as it is a compound having the above structure, and examples thereof include: triethylenediamine, 2-methyltriethylenediamine, quinuclidine, 2-methyl quinuclidine, and the like. Among these, triethylene diamine and 2-methyltriethylene diamine are preferable from the viewpoint of excellent catalyst activity and industrial availability.

As other tertiary amine catalysts, there may be mentioned: <xnotran> N, N, N ', N ' - , N, N, N ', N ' - , N, N, N ', N ", N" - , N, N, N ', N ", N" - - (3- ) , N, N, N ', N ", N" - , N, N, N ', N ' - , (2- ) , , , , N, N- -N ' - (2- ) , N, N- -N ' - (2- ) , ( ) , ( ) ,3- (3-quinuclidinol), N, N, N ', N ' - ,1,3,5- (N, N- ) -S- ,1,8- [5.4.0] -7, N- -N ' - (2- ) , N, N ' - , , N- , N- , 1- ,1,2- , 1- -2- , 1- , </xnotran> N, N-dimethylhexanolamine, N-methyl-N' - (2-hydroxyethyl) piperazine, 1- (2-hydroxyethyl) imidazole, 1- (2-hydroxypropyl) imidazole, 1- (2-hydroxyethyl) -2-methylimidazole, 1- (2-hydroxypropyl) -2-methylimidazole, and the like.

Examples of the aliphatic cyclic amide compound include: delta-valerolactam, epsilon-caprolactam, omega-enantholactam, eta-caprylolactam, beta-propiolactam, and the like. Of these, epsilon-caprolactam is more effective in promoting curing.

The titanium chelate complex is a compound whose catalytic activity is improved by ultraviolet irradiation, and is preferably a titanium chelate complex having an aliphatic or aromatic diketone as a ligand, from the viewpoint of excellent curing acceleration effect. In the present invention, from the viewpoint of further enhancing the effect of the present invention, an alcohol having 2 to 10 carbon atoms is preferably used as the ligand in addition to the aromatic or aliphatic diketone.

In the present invention, the above-mentioned catalysts may be used alone or in combination.

The mass ratio of the catalyst is preferably in the range of 0.001 to 80 parts, more preferably 0.01 to 70 parts, based on 100 parts of the mixed liquid of the polyisocyanate composition (B) and the polyol composition (a).

The reactive adhesive of the present invention may be used in combination with a pigment as required. The pigment usable in this case is not particularly limited, and examples thereof include: organic pigments and inorganic pigments such as extender pigments, white pigments, black pigments, gray pigments, red pigments, brown pigments, green pigments, blue pigments, metal powder pigments, luminescent pigments and pearl pigments described in the handbook of coating materials 1970 (edited by the japan society for coating industries), and plastic pigments can be mentioned. Specific examples of these colorants are disclosed in various forms, and examples of the organic pigment include: benzidine Yellow (Benzidine Yellow), hansa Yellow (Hansa Yellow), raked (12524611248412489) 4R; soluble azo pigments such as Raked C', magenta 6B (Carmine 6B), and purplish red 10 (Bordeaux 10); various (copper) Phthalocyanine-based pigments such as Phthalocyanine Blue (Phthalocyanine Blue) and Phthalocyanine Green (Phthalocyanine Green); various chlorine-colored lakes such as rose bengal Lake (Rhodamine Lake) and Methyl Violet Lake (Methyl Violet Lake); various medium dye-based pigments such as Quinoline Lake (Quinoline Lake) and fixed Sky Blue (Fast Sky Blue); various vat dye-based pigments such as anthraquinone-based pigments, thioindigo-based pigments, and perinone-based pigments; various quinacridone pigments such as cinquaa Red B; various Dioxazine pigments such as Dioxazine Violet (Dioxazine Violet); various azo condensation pigments such as Cromophtal; nigrosine and the like.

Examples of the inorganic pigment include: various chromates such as chrome yellow, zinc chromate, molybdate orange, and the like; various ferrocyanide compounds such as prussian blue; various metal oxides such as titanium oxide, zinc white, mapico Yellow, iron oxide, red iron oxide, green chromium oxide, and zirconium oxide; various sulfides or selenides such as cadmium yellow, cadmium red, and mercury sulfide; various sulfates such as barium sulfate and lead sulfate; various silicates such as calcium silicate and ultramarine; various carbonates such as calcium carbonate and magnesium carbonate; various phosphates such as cobalt violet and manganese violet; various metal powder pigments such as aluminum powder, gold powder, silver powder, copper powder, bronze powder, brass powder, and the like; these metallic flake pigments, mica flake pigments; metal pigments in the form of metal oxide-coated mica, flake pigments, mica-like iron oxide pigments, and the like, and pearlescent pigments; graphite, carbon black, and the like.

Examples of the extender pigment include: precipitated barium sulfate, paris White (powdered \12372), precipitated calcium carbonate, heavy calcium carbonate, gypsum rubrum, alumina White (Alumina White), silica, hydrous micro-powder silica (White carbon), ultrafine anhydrous silica (Aerosil), silica sand (silica sand), talc, precipitated magnesium carbonate, bentonite, clay, kaolin, loess, and the like.

Further, as the plastic pigment, for example, there can be mentioned: "Grandoll PP-1000" and "PP-2000S" manufactured by DIC corporation.

The pigment used in the present invention is excellent in durability, weather resistance and appearance, and is preferably an inorganic oxide such as titanium oxide or zinc white as a white pigment or carbon black as a black pigment.

The mass ratio of the pigment used in the present invention is preferably 1 to 400 parts by mass, more preferably 10 to 300 parts by mass, based on 100 parts by mass of the total of the isocyanate component B and the polyol component a, because of its excellent adhesiveness, blocking resistance, and the like.

(adhesion promoter)

In addition, the reactive adhesive used in the present invention may be used in combination with an adhesion promoter. Examples of the adhesion promoter include: silane coupling agents, titanate coupling agents, aluminum coupling agents, and epoxy resins.

Examples of the silane coupling agent include: aminosilanes such as γ -aminopropyltriethoxysilane, γ -aminopropyltrimethoxysilane, N- β (aminoethyl) - γ -aminopropyltrimethyldimethoxysilane, and N-phenyl- γ -aminopropyltrimethoxysilane; epoxy silanes such as beta- (3, 4-epoxycyclohexyl) ethyltrimethoxysilane, gamma-glycidoxypropyltrimethoxysilane and gamma-glycidoxypropyltriethoxysilane; vinyl silanes such as vinyltris (β -methoxyethoxy) silane, vinyltriethoxysilane, vinyltrimethoxysilane and γ -methacryloxypropyltrimethoxysilane; hexamethyldisilazane, gamma-mercaptopropyltrimethoxysilane, and the like.

Examples of the titanate-based coupling agent include: titanium tetraisopropoxide, titanium tetra-n-butoxide, butyl titanate dimer, tetrastearyl titanate, titanium acetylacetonate, titanium lactate, tetraoctanediol titanate, titanium lactate, titanium tetrastearate, and the like.

Examples of the aluminum-based coupling agent include: acetoalkoxyaluminum diisopropoxide (Acetoakoxy aluminum diisopropyrate), and the like.

As the epoxy resin, there can be mentioned: various commercially available epoxy resins such as Epi-Bis type, novolak type, β -methylepichlorohydrin type, cyclic oxirane type, glycidyl ether type, glycidyl ester type, polyglycol ether type, glycol ether type, epoxidized fatty acid ester type, polycarboxylic acid ester type, aminocyclopropyl type, resorcinol type, etc., tris (2-hydroxyethyl) isocyanurate, neopentyl glycol diglycidyl ether, 1, 6-hexanediol diglycidyl ether, acrylic glycidyl ether, 2-ethylhexyl glycidyl ether, phenyl glycidyl ether, phenol glycidyl ether, p-tert-butyl glycidyl ether, diglycidyl adipate, diglycidyl phthalate, glycidyl methacrylate, butyl glycidyl ether, etc., are generally used.

(other additives)

The reactive adhesive used in the present invention may contain other additives than those described above, if necessary. As additives, for example, there can be used: leveling agents, inorganic fine particles such as colloidal silica and alumina sol, polymethyl methacrylate-based organic fine particles, defoaming agents, anti-sagging agents, wetting and dispersing agents, viscosity modifiers, ultraviolet absorbers, metal deactivators, peroxide decomposers, flame retardants, reinforcing agents, plasticizers, lubricants, rust inhibitors, fluorescent whitening agents, inorganic heat ray absorbers, flame retardants, antistatic agents, dehydrating agents, known and conventional thermoplastic elastomers, tackifiers, phosphoric acid compounds, melamine resins, or reactive elastomers. The content of these additives can be adjusted as appropriate within a range not impairing the function of the reactive adhesive used in the present invention.

These adhesion promoters and additives may be mixed with either the polyisocyanate composition (B) or the polyol composition (a) or may be blended at the time of coating to be used as the third component. Usually, a premix obtained by blending components other than the polyisocyanate composition (B) in the polyol composition (a) in advance is prepared in advance, and the premix and the polyisocyanate composition (B) are mixed just before application.

(laminated body)

The laminate of the present invention is obtained by bonding a plurality of films or papers by a dry lamination method or a non-solvent lamination method using the adhesive of the present invention. In particular, a laminate film obtained by bonding a plurality of films together using the adhesive of the present invention is referred to as a laminate film. The film to be used is not particularly limited, and a film suitable for the purpose may be appropriately selected. For example, as food packaging materials, there are: polyolefin films such as polyethylene terephthalate (PET) films, polystyrene films, polyamide films, polyacrylonitrile films, polyethylene films (LLDPE: low density polyethylene films, HDPE: high density polyethylene films), polypropylene films (CPP: unstretched polypropylene films, OPP: biaxially stretched polypropylene films), and plastic films (also referred to as polymer films) such as polyvinyl alcohol films and ethylene-vinyl alcohol copolymer films.

The film may be one to which a stretching treatment is applied. As a stretching treatment method, generally, a resin is melt-extruded by an extrusion film-forming method or the like to be formed into a sheet, and then simultaneously biaxially stretched or sequentially biaxially stretched. In the case of sequential biaxial stretching, the stretching treatment in the longitudinal direction is usually performed first, and then the stretching in the transverse direction is performed. Specifically, a method of combining longitudinal stretching using a speed difference between rolls and transverse stretching using a tenter is often used.

Alternatively, the following may be used in combination: a film in which a vapor deposition layer of a metal such as aluminum, a metal oxide such as silica or alumina, or a barrier film containing a gas barrier layer such as polyvinyl alcohol, an ethylene-vinyl alcohol copolymer or vinylidene chloride is laminated. By using such a film, a laminate having barrier properties against water vapor, oxygen, alcohols, inert gases, volatile organic compounds (fragrance), and the like can be produced.

In order to form an adhesive layer free from defects such as film shortage and shrinkage (lubricating), the film surface may be subjected to various surface treatments such as flame treatment and corona discharge treatment as necessary.

Alternatively, the laminate of the present invention can be obtained by: the adhesive of the present invention is applied as an adhesive auxiliary agent (anchor coating agent) to a film through a laminator, and after a curing reaction, the melted polymer material is laminated through an extruder (extrusion lamination method). The film may be the same as the film used in the dry lamination method or the non-solvent lamination method. As the molten polymer material, polyolefin-based resins such as low-density polyethylene resin, linear low-density polyethylene resin, ethylene-vinyl acetate copolymer resin and the like are preferable.

More specific examples of the structure of the laminate include:

(1) Substrate film 1/adhesive layer 1/sealing film

(2) Substrate film 1/adhesive layer 1/metal vapor-deposited unstretched film

(3) Base film 1/adhesive layer 1/metal vapor-deposited stretched film

(4) Transparent evaporation stretched film/adhesive layer 1/sealing film

(5) Substrate film 1/adhesive layer 1/substrate film 2/adhesive layer 2/sealing film

(6) Substrate film 1/adhesive layer 1/metal vapor-deposited stretched film/adhesive layer 2/sealing film

(7) Substrate film 1/adhesive layer 1/transparent evaporation-coated stretched film/adhesive layer 2/sealing film

(8) Substrate film 1/adhesive layer 1/metal layer/adhesive layer 2/sealing film

(9) Substrate film 1/adhesive layer 1/substrate film 2/adhesive layer 2/metal layer/adhesive layer 3/sealing film

(10) Substrate film 1/adhesive layer 1/metal layer/adhesive layer 2/substrate film 2/adhesive layer 3/sealing film

And the like, without being limited thereto.

As the base film 1 used in the structure (1), there can be mentioned: an OPP film, a PET film, a nylon film, and the like. As the base film 1, there can be used: a base film 1 is applied with a coating for the purpose of enhancing gas barrier properties, ink receptivity when a printing layer described later is provided, and the like. Commercially available products of the coated base film 1 include: K-OPP film, K-PET film, etc. The adhesive layer 1 is a cured coating film of the adhesive of the present invention. Examples of the sealing film include: CPP films, LLDPE films, and the like. The printed layer may be provided on the side of the substrate film 1 closer to the adhesive layer 1 (when the substrate film 1 to which the coating agent is applied is used, the side of the coating layer closer to the adhesive layer 1). The printing layer can be formed by a common printing method conventionally used for printing on a polymer film, using various printing inks such as gravure ink, flexographic ink, lithographic ink, stencil ink, and inkjet ink.

The base film 1 used in the structures (2) and (3) includes: OPP films, PET films, and the like. The adhesive layer 1 is a cured coating film of the adhesive of the present invention. As the metal deposition unstretched film, there can be used: applying a VM-CPP film formed by evaporating metals such as aluminum and the like to the CPP film; as the metal deposition stretched film, there can be used: a VM-OPP thin film formed by vapor deposition of a metal such as aluminum is applied to the OPP thin film. A printed layer may be provided on the surface of the base film 1 on the side of the adhesive layer 1, similarly to the structure (1).

As the transparent vapor-deposited stretched film used in the structure (4), there can be mentioned: a film formed by vapor deposition of silica or alumina is applied to an OPP film, a PET film, a nylon film, or the like. A thin film coated on the deposition layer for the purpose of protecting an inorganic deposition layer of silica or alumina, or the like can be used. The adhesive layer 1 is a cured coating film of the adhesive of the present invention. The sealing film may be the same as that of the structure (1). The printing layer may be provided on the surface of the transparent vapor-deposited stretched film on the side of the adhesive layer 1 (when a coating is applied to the inorganic vapor-deposited layer, the surface on the side of the adhesive layer 1 of the coating layer). The printing layer is formed in the same manner as in the structure (1).

The base film 1 used in the structure (5) may be a PET film. The base film 2 may be a nylon film. At least one of the adhesive layer 1 and the adhesive layer 2 is a cured coating film of the adhesive of the present invention. The sealing film may be the same as in the structure (1). A printed layer may be provided on the surface of the base film 1 on the side of the adhesive layer 1, in the same manner as in the configuration (1).

The base film 1 of the structure (6) is the same as those of the structures (2) and (3). Examples of the metal deposition stretched film include: VM-OPP film and VM-PET film formed by vapor deposition of metal such as aluminum are applied on OPP film and PET film. At least one of the adhesive layer 1 and the adhesive layer 2 is a cured coating film of the adhesive of the present invention. The sealing film may be the same as in the structure (1). A printed layer may be provided on the surface of the base film 1 on the side of the adhesive layer 1, in the same manner as in the configuration (1).

The base film 1 of the structure (7) may be a PET film. The transparent vapor-deposited stretched film may be the same as that of the structure (4). At least one of the adhesive layers 1 and 2 is a cured coating film of the adhesive of the present invention. The sealing film may be the same as in the structure (1). A printed layer may be provided on the surface of the base film 1 on the side of the adhesive layer 1, similarly to the structure (1).

The base film 1 of the structure (8) may be a PET film. Examples of the metal layer include aluminum foil. At least one of the adhesive layers 1 and 2 is a cured coating film of the adhesive of the present invention. The sealing film may be the same as that of the structure (1). A printed layer may be provided on the surface of the base film 1 on the side of the adhesive layer 1, in the same manner as in the configuration (1).

Examples of the base film 1 having the structures (9) and (10) include a PET film. The base film 2 may be a nylon film. Examples of the metal layer include aluminum foil. At least one of the adhesive layers 1,2, and 3 is a cured coating film of the adhesive of the present invention. The sealing film may be the same as in the structure (1). A printed layer may be provided on the surface of the base film 1 on the side of the adhesive layer 1, similarly to the structure (1).

When the laminate of the present invention includes at least one of a metal vapor-deposited film, a transparent vapor-deposited film, and a metal layer, the adhesive layer in contact with the metal vapor-deposited layer, the transparent vapor-deposited layer, and the metal layer is preferably a cured coating film of the adhesive of the present invention.

When the adhesive of the present invention is a solvent type, the adhesive of the present invention is applied to a film material serving as a base material using a roll such as a gravure roll, the organic solvent is volatilized by heating in an oven or the like, and then another base material is bonded to obtain the laminate of the present invention. It is preferable to perform a curing treatment after lamination. The curing temperature is preferably from room temperature to 80 ℃ and the curing time is preferably from 12 to 240 hours.

When the adhesive of the present invention is a solvent-free adhesive, the adhesive of the present invention, which is previously heated to about 40 to 100 ℃, is applied to a film material serving as a base material using a roll such as a gravure roll, and then another base material is immediately bonded to obtain the laminate of the present invention. It is preferable to perform a curing treatment after lamination. The curing temperature is preferably from room temperature to 70 ℃, and the curing time is preferably from 6 to 240 hours.

When the adhesive of the present invention is used as an adhesive auxiliary agent, the adhesive auxiliary agent of the present invention is applied to a film material serving as a base material using a roll such as a gravure roll, the organic solvent is volatilized by heating in an oven or the like, and then the melted polymer material is laminated by an extruder to obtain a laminate of the present invention.

The amount of the adhesive applied was appropriately adjusted. In the case of a solvent-based adhesive, the amount of the solid content is 1g/m, for example ² Above and 10g/m ² Hereinafter, it is preferably 1g/m ² Above and 5g/m ² The following adjustment is made. In the case of a solvent-free adhesive, the amount of the adhesive applied is 1g/m ² Above and 10g/m ² The amount of the surfactant is preferably 1g/m or less ² Above and 5g/m ² The following is an example.

When the adhesive of the present invention is used as an adhesion auxiliary agent, the amount of the coating is 0.03g/m ² Above and 0.09g/m ² The following (solid content) is an example.

The laminate of the present invention may further contain other films and substrates in addition to the above-described structures (1) to (10). As the other substrate, in addition to the stretched film, the unstretched film, and the transparent vapor-deposited film, a porous substrate such as paper, wood, and leather described later can be used. The adhesive used for bonding other substrates may or may not be the adhesive of the present invention.

As the paper, a known paper base can be used without particular limitation. Specifically, the natural fibers for papermaking such as wood pulp are used and manufactured by a known papermaking machine, and the papermaking conditions are not particularly limited. Examples of natural fibers for papermaking include: wood pulp such as softwood pulp and hardwood pulp, non-wood pulp such as manila pulp, sisal pulp and flax pulp, and pulp obtained by chemically modifying these pulps. As the kind of pulp, there can be used: chemical pulp, pulp (grand pulp), chemical pulp, thermomechanical pulp, and the like obtained by a sulfate digestion method, an acid, neutral, and alkali sulfite digestion method, a sodium carbonate digestion method, and the like.

In addition, it is also possible to use: various commercially available forest papers, coated papers, paper liners, impregnated papers, corrugated papers, paper boards, and the like. Further, a printed layer may be provided on the outer surface or the inner surface of the paper layer as necessary.

The "other layers" may contain known additives, stabilizers, for example: antistatic agents, easy adhesion coating agents, plasticizers, lubricants, antioxidants, and the like. In addition, in order to improve adhesion when the film is laminated with another material, the "another layer" may be a layer obtained by subjecting the surface of the film to corona treatment, plasma treatment, ozone treatment, chemical treatment, solvent treatment, or the like as a pretreatment.

As described above, in order to maximize the effect of the present invention that a laminate having high adhesiveness and an excellent appearance after lamination processing can be obtained even under high-speed coating conditions, it is preferable that the adhesive of the present invention is first applied to a plastic film, and then the adhesive surface is bonded to another plastic film or a porous substrate other than the plastic film, for example, a transparent vapor deposition film, paper, wood, leather, or the like, to obtain a laminate.

The laminate of the present invention can be suitably used for various applications, and is suitably used for, for example, packaging materials for foods, pharmaceuticals, living goods, covering materials, paper tableware such as paper straws, napkins, paper spoons, paper trays and paper cups, barrier materials, roofing materials, solar cell panel materials, battery packaging materials, window materials, outdoor flooring materials, illumination protection materials, automobile members, signboards, labels and other outdoor industrial applications, decorative sheets used in injection molding and decoration methods, washing liquid detergents, kitchen liquid detergents, bath liquid soaps, liquid shampoos, liquid hair tonics and other packaging materials.

< packaging Material >

The laminate of the present invention is useful as a multilayer packaging material for the purpose of protecting foods, pharmaceuticals, and the like. When used as a multilayer packaging material, the layer structure thereof may be changed depending on the contents, the use environment, and the use form. The package of the present invention may be provided with an easy-opening treatment and a resealable structure.

The packaging material of the present invention is obtained by using the laminate of the present invention, laminating the sealing films of the laminate in the facing direction, and heat-sealing the peripheral end portions thereof to form a bag shape. As the bag-making method, there can be mentioned: the laminate of the present invention is folded or laminated so that the inner layers (surfaces of the sealing films) face each other, and the peripheral ends thereof are heat sealed in a form such as a side seal type, a double seal type, a triple seal type, a four-side seal type, a letter seal type, a half seal type, a seal type with a folded edge, a flat seal type, a square seal type, a double seal type, or another heat seal type. The packaging material of the present invention can take various forms depending on the contents, the use environment, and the use form. A self-supporting packaging material (self-supporting bag) or the like may be used. The heat sealing can be performed by a known method such as a bar seal, a rotary roll seal, a tape seal, a flash seal, a high-frequency seal, or an ultrasonic seal.

The packaging material of the present invention is filled with contents through its opening, and then the opening is heat-sealed to produce a product using the packaging material of the present invention. Examples of the contents to be filled include food products: rice-based confectionery, bean-based confectionery, nuts, hard biscuits (cookies), wafers, marshmallows, pies, half-cooked cakes, candies, snack bars, bread, snack noodles, instant noodles, dry noodles, pasta, aseptically packaged cooked rice, japanese rice, porridge, bagged rice cakes, staple foods such as cereal foods, pickles, boiled beans, natto, miso, frozen tofu, nameko mushrooms, konjac, processed yam, jam, peanut butter, salads, frozen vegetables, processed potato products, ham, bacon, sausage, processed chicken, processed pickled beef, ham, sausage, etc., processed meat products of livestock products such as ham, meat, sausage, meat, and meat aquatic product refined product, fish plate, sea sedge, sweet seafood (tsukudani), fillet, seafood pickled product (Shiokara), smoked salmon, spicy processed product of Pseudostellaria heterophylla, fruit meat such as peach, orange, pineapple, apple, american pear, cherry, vegetables such as corn, asparagus, mushroom, onion, carrot, white radish, potato, frozen cooked food such as hamburger, meat ball, aquatic fried product, dumpling, cola cake, etc., prepared food such as refrigerated cooked food, dairy product such as butter, margarine, cheese, cream, instant milk essence, formula milk powder for infant care, liquid flavoring agent, instant curry, pet food, etc.

Further, as a non-food product, it can be used as a pharmaceutical product such as a cigarette, a disposable warming pack, and an infusion bag, a liquid detergent for washing, a liquid detergent for kitchen use, a liquid detergent for bath, a liquid soap for bath, a liquid shampoo, a liquid hair cream, a cosmetic such as a lotion and an emulsion, a vacuum insulator, and various packaging materials such as a battery.

Examples

The contents and effects of the present invention will be described in more detail below with reference to examples, but the present invention is not limited to the examples below.

Synthesis examples 1 to 16: process for producing polyol composition (A)

(Synthesis example 1)

Method for synthesizing polyester polyol (a 1-1)

Into a glass four-necked flask of 2 l equipped with a stirring blade, a temperature sensor, a nitrogen gas inlet tube and a rectifying column, 35.2g of ethylene glycol, 83.3g of neopentyl glycol, 105.3g of 1, 6-hexanediol, 124.0g of adipic acid, 126.4g of isophthalic acid, 63.2g of terephthalic acid, 96.5g of dimer acid, 73.1g of a solution containing 1X 10 carbon atoms ^-6 An average particle diameter of 1X 10 mass% or more and less than 1 mass% ^-3 Fine PET pellets (A) having a diameter in the range of mm to 0.5mm and 0.2g of dibutyltin oxide as a polymerization catalyst. The temperature was raised to 250 ℃ while gradually raising the temperature under normal pressure nitrogen flow and carrying out dehydration reaction, and after reaction was carried out at 250 ℃ for 2 hours, when it was confirmed that the contents became transparent and the top temperature of the rectifying column became 80 ℃ or lower, the rectifying column was disassembled and switched to a glass condenser, and the line was connected from the nitrogen inlet pipe to a vacuum pump to carry out condensation reaction under reduced pressure of 50Torr for 5 hours. When the temperature was decreased to 130 ℃ after reaching a predetermined acid value and viscosity, ethyl acetate was poured into the mixture using a dropping funnel and the mixture was diluted to obtain a polyester polyol (a 1-1). The weight fraction of PET pellets when charged with the raw materials, the acid value of the polyester polyol (a 1-1) in terms of solids, and the hydroxyl value in terms of solids are shown in Table 1.

(Synthesis examples 2) to 7

Polyester polyols (a 1-2) to (a 1-7) were synthesized in the same manner as in (synthetic example 1) except that the raw materials shown in Table 1 were used. The weight fraction of PET pellets when charged with the raw materials, and the acid value and hydroxyl value in terms of solids of the polyester polyols (a 1-2) to (a 1-7) are shown in Table 1.

(Synthesis example 8)

Method for synthesizing polyester polyol (a 1-8)

Into a glass four-necked flask of 2 liters equipped with a stirring blade, a temperature sensor, a nitrogen gas inlet tube and a rectifying column, 35.2g of ethylene glycol, 83.3g of neopentyl glycol, 105.3g of 1, 6-hexanediol, 124.0g of adipic acid, 126.4g of isophthalic acid, 63.2g of terephthalic acid, 96.5g of dimer acid, 73.1g of PET pellets B containing no fine particles and 0.2g of dibutyltin oxide as a polymerization catalyst were charged. The temperature was raised to 250 ℃ under a nitrogen atmosphere and the dehydration reaction was carried out while gradually raising the temperature to 250 ℃, and after 2 hours of reaction at 250 ℃, when it was confirmed that the contents were transparent and the temperature at the top of the rectifying column was 80 ℃ or lower, the rectifying column was removed and switched to a glass condenser, and the line was connected from the nitrogen introduction pipe to a vacuum pump to carry out a condensation reaction for 5 hours under a reduced pressure of 50 Torr. When the acid value and viscosity reached the predetermined values, the temperature was reduced to 130 ℃ and ethyl acetate was poured into the mixture using a dropping funnel to dilute the mixture. Thereafter, 0.03g of polyethylene powder (FLO-BEADS CL-2080 manufactured by Sumitomo Seiko Co., ltd.) was charged and stirred until uniform, to obtain polyester polyols (a 1 to 8). The weight fraction of PET pellets when charged with the raw materials, the acid value of the polyester polyol (a 1-8) in terms of solids, and the hydroxyl value in terms of solids are shown in Table 1.

(Synthesis example 9)

Method for synthesizing polyester polyol (a 1-9)

The synthesis was carried out in the same manner as in (synthesis example 8) using the raw materials shown in Table 1. The styrene polymer (Fuji film and Wako pure chemical industries, ltd.) was finely pulverized and then charged in the same manner as in Synthesis example 8 to obtain polyester polyols (a 1-9). The weight fraction of PET pellets when the starting materials were charged, and the acid value and hydroxyl value of the polyester polyol (a 1-9) in terms of solids are shown in Table 1.

(Synthesis example 10)

Method for synthesizing polyester polyol (a 1-10)

Polyester polyols (a 1 to 10) were synthesized in the same manner as in (synthetic example 8) except that the raw materials shown in table 1 were used. The weight fraction of PET pellets when the raw material (cellulose powder (Fuji film and Wako pure chemical industries, ltd.)) was charged, the acid value in terms of solids of the polyester polyol (a 1-10), and the hydroxyl value in terms of solids are shown in Table 1.

(Synthesis example 11)

Method for synthesizing polyester polyurethane polyol (a 2-1)

Into a 2-liter glass four-necked flask equipped with a stirring blade, a temperature sensor, a nitrogen gas inlet tube and a glass condenser tube were charged 300.0g of the polyester polyol (a 1-1) and 0.1g of dibutyltin dilaurate as a polymerization catalyst. Once the temperature was raised to 60 ℃ under a nitrogen stream at normal pressure, 9.0g of isophorone diisocyanate was charged and heated to 80 ℃ and urethanization was carried out at 80 ℃ for 5 hours. After confirming that the viscosity reached a predetermined level and the residual isocyanate content was 0.05% or less, the temperature was lowered to 50 ℃ and the solid content was appropriately adjusted with ethyl acetate to obtain polyester-urethane polyol (a 2-1). The acid value and the hydroxyl value in terms of solids of the resulting polyester-polyurethane polyol (a 2-1) are shown in Table 3.

(Synthesis examples 12) to 16)

Polyester polyurethane polyols (a 2-2) to (a 2-6) were synthesized in the same manner as in (synthetic example 11) except that the raw materials shown in Table 2 were used. The acid value and the hydroxyl value in terms of solids of the polyester-polyurethane polyols (a 2-2) to (a 2-6) obtained are shown in Table 2.

In tables 1 and 2, the unit of the amount charged is g. In addition, the blank field is unmatched.

[ Table 1]

[ Table 2]

(examples and comparative examples)

The polyol compositions (a) obtained in examples and comparative examples were adjusted to have particle sizes and contents shown in tables 3 and 4 by appropriately diluting the compositions with ethyl acetate and then subjecting the compositions to filtration or the like.

The content of the fine particles shown in tables 3 and 4 is a value obtained by measuring a Turbidity in Nephelometric Turbidity units "NTU (Nephelometric turbidimetry Unit)" using a turbidimeter (model Lavibond TB300IR manufactured by Tintometer Group) for a solution in which the polyester polyol (a) is diluted with ethyl acetate to have a solid content of 60%, converting the Turbidity into a mass% according to a calculation formula of 1ntu =1mg/L =1ppm, and converting the obtained value into a solid content.

The reactive adhesives used in the examples and comparative examples were prepared by blending the polyol composition (a) and the polyisocyanate composition (B) in the ratios shown in tables 3 and 4. In addition, 3-functional polyisocyanate (DICDRY KW-75 manufactured by DIC corporation, solid content 75%) obtained by adding tolylene diisocyanate to trimethylolpropane and a biuret product of hexamethylene diisocyanate (90% solid content manufactured by DIC Graphics corporation) were used as the polyisocyanate composition (B). The evaluation was carried out according to the criteria shown below. The results are shown in tables 3 and 4, respectively.

(evaluation)

(storage stability of polyol composition (A))

The polyol compositions (a) obtained in examples and comparative examples were diluted with ethyl acetate to 60% solid content, collected in a transparent glass bottle so as not to cause bubbles, sealed, and then stored in a dryer at 40 ℃ for 1 month. The appearance after storage was observed, and the following evaluation was made based on the degree of precipitation of fine particles.

Evaluation ∈: no precipitate was seen at all.

Evaluation ∘: precipitation was slightly visible, but the appearance of the resin solution was not changed.

Evaluation Δ: precipitation was clearly seen and the appearance of the resin solution was visibly changed.

Evaluation x: most of the particles precipitated and the appearance of the resin solution changed greatly.

(appearance of laminate)

The Ny film (commercially available nylon film) as the first plastic film layer was coated at a coating weight of 3 to 3.5g/m at a processing speed of 250m/min using Dry Laminator (Dry Lami Test Coater, kyoto mechanical design Co., ltd.) as a Laminator ² After coating the adhesive of example or comparative example, VMPET (commercially available aluminum vapor deposition unstretched polyethylene terephthalate film) as a second plastic film layer was laminated to obtain a laminate. The appearance of the film immediately after lamination (presence or absence of wrinkles, floating due to bubbles, or defects such as tunneling due to variations between films) was visually observed.

Evaluation criteria

Very good: the number of bubbles is 0 and no wrinkles or tunneling

O: the number of bubbles is 1-4 and no wrinkles or tunneling

O-: 5-9 bubbles without wrinkles or tunneling

And (delta): the number of the bubbles is 10-16, and wrinkles and tunneling partially occur

X: the number of the bubbles is 17 or more, and wrinkles and tunnels are generated at a plurality of positions

In tables 3 and 4, the unit of the amount of incorporation is g, and the blank field is no incorporation.

[ Table 3]

[ Table 4]

[ Table 5]

The polyol composition (a) used in (examples 1) to 17) shows little sedimentation with time, and when used as an adhesive, a laminate having an excellent appearance after lamination processing can be obtained. On the other hand, precipitation with time or appearance defects after lamination processing occurred in (comparative examples 1) to 7.

(example of laminate)

( The method for producing the laminate for retort resistance test: structure comprising aluminum foil )

The adhesive was mixed in the proportions shown in the table, and the amount of the adhesive applied was 3.5g/m as a solid content ² The right and left systems were applied to a 12 μm thick PET film, the solvent was dried, and the adhesive-applied surface of the film was laminated and bonded to a 15 μm thick nylon film by a laminator to laminate the film. Then, the amount of the adhesive is set toSolid content 3.5g/m ² The left and right patterns were applied to the nylon surface of the laminate, and after drying the solvent, the adhesive-applied surface of the laminate was bonded and laminated to an aluminum foil having a film thickness of 9 μm by means of a laminator. Further, the solid content was 3.5g/m ² In the right and left embodiments, an adhesive was applied to the surface opposite to the adhesive-applied surface of the aluminum foil, and after drying the solvent, the adhesive-applied surface of the laminate was bonded and laminated to a heat-resistant non-oriented polypropylene film (heat-resistant CPP) having a film thickness of 70 μm using a laminator. Thereafter, the resultant was stored in a thermostatic bath at 40 ℃ for 3 days to obtain a laminate.

(method of producing laminate for boiling resistance test)

The adhesive was mixed in the ratio shown in the table, and the coating amount was 3.0g/m as a solid content ² In the right and left embodiments, an adhesive is applied to a deposition layer of a PET film having a film thickness of 12 μm, a nylon (Ny) film having a film thickness of 15 μm, or a transparent deposition film having a film thickness of 15 μm, and after drying a solvent, the coated surface of the adhesive is laminated and bonded to a linear low density polyethylene film (LLDPE) having a film thickness of 60 μm by a laminator to laminate. Thereafter, the resultant was stored in a thermostatic bath at 40 ℃ for 3 days to obtain a laminate.

(method of producing laminate for retort resistance test)

The adhesive was mixed in the ratio shown in the table, and the amount of the adhesive applied was 3.0g/m as a solid content ² In the right and left embodiments, an adhesive is applied to a deposition layer of a PET film having a film thickness of 12 μm, a nylon (Ny) film having a film thickness of 15 μm, or a transparent deposition film having a film thickness of 15 μm, and after drying a solvent, the coated surface of the adhesive is laminated and bonded to a heat-resistant unstretched polypropylene film (heat-resistant CPP) having a film thickness of 70 μm using a laminator, thereby laminating the layers. Thereafter, the resultant was stored in a thermostatic bath at 40 ℃ for 3 days to obtain a laminate.

(method of measuring Normal State lamination Strength)

Immediately after the production of the laminate, the laminate was cut out in a width of 15mm, and the adhesive strength (T-peel) was measured at a peel speed of 300mm/min using a tensile tester (unit: N/15 mm).

(lamination Strength and appearance after boiling treatment)

The laminate for the boiling resistance test was cut at 120mm × 220mm, and was folded so that LLDPE was positioned inside, and heat-sealed at 1atm and 180 ℃ for 1 second to prepare a bag (pouch). 1/1/1 sauce (meat paste: vegetable oil: vinegar = 1: 1) was added as the content.

The filled bags were boiled at 98 to 60 minutes to remove the contents, and the T-peel strengths between PET/LLDPE, ny/LLDPE and transparent vapor-deposited PET/LLDPE were measured. The appearance of each bag after the removal was observed, and the following evaluation was performed by the presence or absence of delamination.

Evaluation ∘: without delamination

Evaluation Δ: delamination site is 5 or less

Evaluation x: the delamination site is more than 6

(lamination strength and appearance after retort treatment)

The laminate for the retort resistance test was cut out to 120mm × 220mm, folded so that the heat-resistant CPP was on the inside, and heat-sealed at 1atm, 180 ℃ for 1 second to prepare a bag. 1/1/1 sauce (meat paste: vegetable oil: vinegar = 1: 1) was added as the content.

The filled bag was subjected to a retort treatment under a condition of 125 to 30 minutes (vapor type), the content was removed, and the strength by T-type peeling between PET/CPP, ny/CPP, transparent vapor-deposited PET/CPP, and aluminum foil/CPP was measured. The appearance of each bag after removal was observed, and the following evaluation was made by the presence or absence of delamination.

Evaluation ∘: without delamination

Evaluation Δ: the delamination site is 5 or less

Evaluation x: the delamination part is more than 6

[ Table 6]

[ Table 7]

In tables 2 to 7, abbreviations are as follows.

KW-75: 3-functional polyisocyanate obtained by adding toluene diisocyanate to trimethylolpropane, solid content 75%

KR-90: biuret product of hexamethylene diisocyanate

Lami strength: lamination strength

PET: polyethylene terephthalate

LLDPE: laminate of linear low density polyethylene

Ny: nylon

PET-AL: laminate of polyethylene terephthalate and aluminum

CPP: non-stretched polypropylene film

/: expressed as an adhesive layer

Delami (1248712521\ 125111: delamination of

F-cut: film cutting (indicating sufficient adhesive strength)

As a result, the polyol composition (a) used in (example 1) to (example 17) can obtain sufficient adhesive strength even when used as an adhesive.

Claims (8)

1. A reactive adhesive comprising a polyol composition (A) and a polyisocyanate composition (B), wherein the polyol composition (A) comprises a polyester polyol (A1) and/or a polyester polyurethane polyol (A2) and has an average particle diameter of 1 x 10 ^-3 A fine particle (C) having a diameter of not less than 0.5mm, wherein the polyester polyol (A1) is a reaction product obtained by charging polyethylene terephthalate, a polyol and a polybasic acid at one time, the polyester urethane polyol (A2) is a reaction product of the polyester polyol (A1) and an isocyanate compound,

1X 10 relative to the total resin solids content of the polyol composition (A) ^-6 The fine particles (C) are contained in an amount of not less than 0.1% by mass.

2. The reactive adhesive according to claim 1, wherein the ratio of the polyethylene terephthalate in the charged raw material of the polyester polyol (A1) is 5 to 50% by mass.

3. The reactive adhesive according to claim 1 or 2, wherein the polybasic acid is a dimer acid, and the ratio of the dimer acid in the charged raw materials of the polyester polyol (A1) is 5 to 20% by mass.

4. A laminate comprising a plurality of films or papers bonded to each other with an adhesive, wherein the adhesive is the reactive adhesive according to any one of claims 1 to 3.

5. A laminate comprising a film or paper having a plurality of printed layers bonded thereto with an adhesive, wherein the adhesive is the reactive adhesive according to any one of claims 1 to 3.

6. A package obtained by forming the laminate according to claim 4 or 5 into a bag shape.

7. A method for producing a reactive adhesive according to any one of claims 1 to 3, comprising: a step of adding polyethylene terephthalate, a polyhydric alcohol, and a polybasic acid all at once, reacting them, and then filtering them with a filter to obtain a polyester polyol (A1).

8. A method for producing a reactive adhesive according to any one of claims 1 to 3, comprising: a step of reacting polyisocyanate with polyester polyol (A1) obtained by charging polyethylene terephthalate, a polyol and a polybasic acid at one time and reacting them, and then filtering the reaction product with a filter to obtain polyester polyurethane polyol (A2).